JPH06283160A - Maturing/drying device of electrode plate for lead-acid battery - Google Patents

Maturing/drying device of electrode plate for lead-acid battery

Info

Publication number
JPH06283160A
JPH06283160A JP5071608A JP7160893A JPH06283160A JP H06283160 A JPH06283160 A JP H06283160A JP 5071608 A JP5071608 A JP 5071608A JP 7160893 A JP7160893 A JP 7160893A JP H06283160 A JPH06283160 A JP H06283160A
Authority
JP
Japan
Prior art keywords
electrode plate
aging
air
drying
maturing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP5071608A
Other languages
Japanese (ja)
Inventor
Osamu Maruyama
修 丸山
Takeshi Hirakawa
武 平川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Resonac Corp
Original Assignee
Shin Kobe Electric Machinery Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shin Kobe Electric Machinery Co Ltd filed Critical Shin Kobe Electric Machinery Co Ltd
Priority to JP5071608A priority Critical patent/JPH06283160A/en
Publication of JPH06283160A publication Critical patent/JPH06283160A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Battery Electrode And Active Subsutance (AREA)

Abstract

PURPOSE:To provide a device maturing and drying electrode plate groups constituted of multiple electrode plates in a short period. CONSTITUTION:In a maturing/drying device maturing electrode plate groups 1 constituted of multiple electrode plates, air feed nozzles 5 feeding the air directly to the electrode plate groups 1 are arranged in a maturing/drying chamber 3. When the composition, temperature, humidity, and feed quantity of the air from the air feed nozzles 5 are properly selected, all electrode plate groups 1 in the maturing/drying chamber 3 can be matured in a short period at the same time.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は格子体にペーストを充填
した未化成極板を腰数重ね合わせた極板群を短時間で熟
成、乾燥することが可能な熟成乾燥装置に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an aging drying apparatus capable of aging and drying an electrode plate group in which unformed electrode plates in which a grid is filled with paste are piled up in a number of times in a short time.

【0002】[0002]

【従来の技術】鉛蓄電池用ペースト式未化成極板は、鉛
に一部が酸化された鉛粉と水と希硫酸と必要に応じて合
成樹脂よりなる短繊維、あるいは種々の添加剤とともに
混練してペースト状とし、該ペーストを格子体に充填し
た後予備乾燥し、これを密着して、さらに乾燥機に入れ
て本乾燥することにより作製される。例えば、特開昭5
4−37227号公報(以下「公報1」という)には熟
成室に入れる空気量を管理して熟成時間短縮することが
示され、また特開昭57−180875号公報(以下
「公報2」という)には複数段のラックに未化成極板を
懸垂し、この周囲を通気性および通水性がなく保温性を
有するシートで覆い、ラックの上下には通気性および通
水性を有するシートで覆うことが提案されている。
2. Description of the Related Art A paste-type unformed electrode plate for a lead storage battery is prepared by kneading lead powder in which lead is partially oxidized, water, dilute sulfuric acid and, if necessary, short fibers made of synthetic resin, or various additives. It is made into a paste by filling the grid with the paste, predrying it, adhering it closely, and further putting it in a dryer for main drying. For example, JP-A-5
Japanese Laid-Open Patent Publication No. 4-37227 (hereinafter referred to as "Gazette 1") discloses that the amount of air put into the aging chamber is controlled to shorten the aging time, and Japanese Patent Laid-Open No. 57-180875 (hereinafter referred to as "Gazette 2"). ), A non-polarized electrode plate should be suspended in multiple racks, and the surrounding area should be covered with a sheet that does not have air permeability and water permeability and retains heat, and the top and bottom of the rack should be covered with sheets that have air permeability and water permeability. Is proposed.

【0003】[0003]

【発明が解決しようとする課題】この熟成は格子体と活
物質との密着、活物質強度の向上、活物質中の亀裂発生
防止を目的とするもので、高率放電特性や寿命性能に大
なる関係を有する鉛蓄電池製造工程の中では最も重要な
一工程である。このため、一般的には18h〜3日の時
間を要して行なっている。従って鉛蓄電池の製造には7
〜10日の長時間を要している。近年、この時間を短縮
する要求が強まってきている。これがためには熟成時間
を短縮する必要がある。そこで、この熟成に長時間要し
ている原因を調査した結果、熟成室に多量の極板を入れ
るために、熟成が早く終了するものと、遅く終了するも
のとの差が大きく、最も遅く終了する極板に合わせて熟
成しているために長時間を要していることが明らかにな
った。上記熟成の目的は、極板中の水分を徐々に除去
し、まず格子体を腐食させて該格子体と活物質とを密着
させ、次に極板中の金属鉛を酸化させることである。
The purpose of this aging is to adhere the lattice to the active material, improve the strength of the active material, and prevent cracks from occurring in the active material. It is one of the most important processes in the lead-acid battery manufacturing process having the following relationship. For this reason, it generally takes 18 hours to 3 days. Therefore, 7 is required for manufacturing lead acid batteries.
It takes a long time of 10 days. In recent years, there is an increasing demand for shortening this time. This requires shortening the aging time. Therefore, as a result of investigating the reason why this aging takes a long time, there is a large difference between the one that finishes early and the one that finishes late because of the large number of electrode plates placed in the ripening room, and the one that finishes the most late It has become clear that it takes a long time because it is aged according to the electrode plate to be used. The purpose of the aging is to gradually remove water in the electrode plate, first to corrode the grid body to bring the grid body and the active material into close contact with each other, and then to oxidize the metallic lead in the electrode plate.

【0004】また熟成が遅く終了する極板の原因を調査
した結果、極板中の水分の除去速度が極めて遅いため、
金属鉛の酸化開始時間もこれと共に遅くなることが主な
理由であることが明らかになった。上記極板中の水分の
除去速度が極めて遅い原因は、極板群の周囲の湿度が適
切な値より高い、あるいは極板群の周囲の風速が遅いた
めで、ファンを設ける等の対策を講じて、熟成室内のす
べての極板群の周囲の風速および雰囲気を均一にするよ
うにしているが、その中に入れる極板群の量等によりこ
れらが大幅に変化するので均一化は極めて困難である。
このような欠点を除去するために小さな恒温恒湿槽を多
数個設置して、この中に入れる極板群の量を一定にして
極板群周囲の風速、雰囲気のバラツキを小さくして時間
短縮を図っているが、設備費が高価になる欠点がある。
Further, as a result of investigating the cause of the electrode plate which finishes aging late, the removal rate of water in the electrode plate is extremely slow.
It was clarified that the main reason is that the start time of oxidation of metallic lead is also delayed. The reason why the removal rate of water in the plate is extremely slow is that the humidity around the plate group is higher than an appropriate value or the wind speed around the plate group is slow, so take measures such as installing a fan. Therefore, the wind speed and atmosphere around all the electrode plates in the aging chamber are made uniform, but it is extremely difficult to make them uniform because they greatly change depending on the amount of electrode plates put in it. is there.
In order to eliminate such defects, a number of small constant temperature and humidity chambers are installed, and the amount of electrode plate group put in this is kept constant to reduce the wind speed around the electrode plate group and the variation of the atmosphere to shorten the time. However, there is a drawback that the equipment cost is high.

【0005】一方、熟成後における本乾燥も熟成の場合
と同様に極板群を多量に乾燥機に入れて行なっているの
で、該極板群の乾燥機内での位置により乾燥速度に大き
な差が認められる。このため、乾燥の最も遅い極板群が
乾燥するまで行なうので、乾燥時間が長くなる欠点を有
している。これを解決する手段は上記熟成の場合と同様
であるが、上記熟成と同様な欠点を有することとなる。
このような欠点を解決するための公報1でも多量の極板
を熟成する時に生ずる極板群の熟成時間のバラツキを少
なくする効果は認められない。また公報2ではラックの
段数が少なく、極板枚数が少ない場合には熟成が均一に
起こり、時間も短くなるが、極板枚数が多くなると熟成
時間のバラツキが大きくなる欠点を有している。さらに
前記シートの取り付け、取り外しには多くの工数を必要
とし、複数段ラックを使用する限り極板枚数が多くなる
と、熟成の場合と同様に乾燥時間のバラツキが大きく、
乾燥時間を長く要する欠点を有している。
On the other hand, the main drying after aging is carried out by putting a large number of electrode plates in the dryer as in the case of aging, so that there is a large difference in the drying speed depending on the position of the electrode plates in the dryer. Is recognized. For this reason, since it is performed until the electrode plate group that is the slowest to dry is dried, there is a drawback that the drying time becomes long. The means for solving this is the same as in the case of the above aging, but it has the same drawbacks as the above aging.
Even in the publication 1 for solving such a drawback, the effect of reducing the variation in the aging time of the electrode plate group when aging a large number of electrode plates is not recognized. Further, in Publication 2, when the number of racks is small and the number of electrode plates is small, aging occurs uniformly and the time is shortened. However, when the number of electrode plates is large, the aging time varies greatly. Furthermore, a lot of man-hours are required for attaching and detaching the sheet, and if the number of electrode plates is large as long as a multi-tier rack is used, the variation in the drying time is large as in the case of aging,
It has the drawback of requiring a long drying time.

【0006】[0006]

【課題を解決するための手段】本発明は上記課題を解決
するために、熟成乾燥装置中のペーストを格子体に充填
した極板を重ね合わせた極板群の各段の極板に直接気体
を当てることができる空気送出ノズルを配置させた熟成
乾燥装置により熟成乾燥行うものである。
In order to solve the above-mentioned problems, the present invention provides a method in which a gas in the aging / drying device is directly vaporized to each electrode plate of an electrode plate group in which electrode plates having grids filled with paste are stacked. Aging / drying is performed by an aging / drying device in which an air delivery nozzle capable of hitting is placed.

【0007】[0007]

【作用】熟成乾燥装置の空気送出ノズルにより該装置中
の各段の極板に同一の温度、湿度の気体を供給すること
ができるので、これらの極板はほぼ同一時間で熟成およ
び乾燥が可能となる。さらに、このノズルより送り出す
空気の組成、量、湿度等を任意に変化させることができ
るので、熟成に適した条件あるいは乾燥に適した条件を
選択することにより、短時間で熟成および乾燥させるこ
とができる。
The gas of the same temperature and humidity can be supplied to the electrode plates of each stage in the aging / drying device by the air delivery nozzle, so that these plates can be aged and dried in substantially the same time. Becomes Furthermore, since the composition, amount, humidity, etc. of the air sent out from this nozzle can be arbitrarily changed, it is possible to perform aging and drying in a short time by selecting the conditions suitable for aging or the conditions suitable for drying. it can.

【0008】[0008]

【実施例】本発明の一実施例について説明する。図1に
示すように、ペーストを格子体に充填した後の極板を複
数枚重ね合わせた極板群1を極板懸垂枠2に懸吊し、こ
れを熟成乾燥室3に入れる。該熟成乾燥室3内には空気
送出口4を一定間隔例えば5mmおきに等間隔に設けた
空気送出ノズル5を極板群1の上部に空気が直接当るよ
うに配置する。図2には極板群1と空気送出ノズル5と
の位置関係を示したものである。空気送出ノズル5から
送出された空気は、熟成乾燥室3中の極板群1の各段の
極板に直接当たることによってこれらの極板を同一に熟
成乾燥させ、空気の湿度、温度、組成が変化する。これ
らの空気は空気調整機6で熟成あるいは乾燥に適した条
件の空気に調整されて空気ポンプ7により、再び空気送
出ノズル5を通って極板群1に送出される。
EXAMPLE An example of the present invention will be described. As shown in FIG. 1, an electrode plate group 1 obtained by stacking a plurality of electrode plates after filling a grid with paste is suspended on an electrode plate suspension frame 2 and placed in an aging drying chamber 3. In the aging / drying chamber 3, air delivery nozzles 5 having air delivery ports 4 provided at regular intervals, for example, every 5 mm, are arranged so that the air directly hits the upper part of the electrode plate group 1. FIG. 2 shows the positional relationship between the electrode plate group 1 and the air delivery nozzle 5. The air sent out from the air sending nozzle 5 directly hits the electrode plates of each stage of the electrode plate group 1 in the aging drying chamber 3 so as to age and dry these electrode plates in the same manner, and the humidity, temperature and composition of the air. Changes. These airs are adjusted to air under conditions suitable for aging or drying by an air conditioner 6, and are sent to the electrode plate group 1 again through an air sending nozzle 5 by an air pump 7.

【0009】つぎに本発明による熟成乾燥装置を用いて
熟成乾燥した一例を図3および図4で説明する。常法に
より作製したペーストを鉛合金格子体に充填し、予備乾
燥して水分量を約10%にした極板を複数枚重ね合わせ
た極板群1を構成させ、該極板群1を極板懸垂枠2に上
下二段に懸垂させる。次に上記空気送出ノズル5より温
度40℃、湿度70%の空気を風速3m/sで極板群1
に当てると、図3に示すように上段極板群1A、下段極
板群1Bともに金属鉛の酸化による発熱が30分目から
始まり、2時間30分目に最高温度に到達し、6時間後
には終了して熟成が完了する。この場合の上段極板群1
Aおよび下段極板群1B中の活物質水分量はいずれも4
%であった。
Next, an example of aging and drying using the aging and drying apparatus according to the present invention will be described with reference to FIGS. 3 and 4. A lead alloy grid is filled with a paste prepared by a conventional method, and a plate group 1 is formed by stacking a plurality of electrode plates preliminarily dried to a water content of about 10%. The board suspension frame 2 is suspended vertically in two stages. Next, air having a temperature of 40 ° C. and a humidity of 70% was supplied from the air delivery nozzle 5 at a wind speed of 3 m / s to the electrode plate group 1.
As shown in FIG. 3, heat generation due to the oxidation of metallic lead started in the upper electrode plate group 1A and the lower electrode plate group 1B from the 30th minute, reached the maximum temperature at 2 hours and 30 minutes, and after 6 hours. Ends and ripening is complete. Upper electrode plate group 1 in this case
The water content of the active material in A and the lower electrode group 1B is 4
%Met.

【0010】なお、本実施例で用いた空気送出ノズル5
の空気送出口4を5mmおきに等間隔に設け、風速3m
/s以上で空気を送出することにより、極板群1に均一
に空気を当てることができる。次に同一空気送出ノズル
5により100℃の乾燥空気を5m/sの風速で極板群
1に当てると、図4に示すように約3時間後にはすべて
の極板群1の活物質中の水分量は0.5%以下まで低下
していた。上段極板群1Cおよび下段極板群1Dは極板
群1中の活物質水分量である。
The air delivery nozzle 5 used in this embodiment
The air outlets 4 are installed at regular intervals of 5 mm and the wind speed is 3 m.
The air can be uniformly applied to the electrode plate group 1 by sending out the air at / s or more. Next, when dry air of 100 ° C. is applied to the electrode plate group 1 by the same air delivery nozzle 5 at a wind speed of 5 m / s, as shown in FIG. The water content was reduced to 0.5% or less. The upper electrode plate group 1C and the lower electrode plate group 1D are the active material water content in the electrode plate group 1.

【0011】比較例 比較のために、上記実施例と同一条件で構成した極板群
を空気送出ノズルを設けていない上記実施例と同一寸法
からなる従来の熟成乾燥室に入れて熟成および乾燥を行
なった。この場合の熟成乾燥室に入れる空気の温度、湿
度、量は上記実施例と同一にした。また、このときの熟
成乾燥室の空気の撹拌は通常一般的に行なわれているよ
うに、上部と側部にファンを設置して行なった。なお、
ここでは熟成前の極板の活物質水分量も上記実施例と同
様に10%とした。その結果、図5に示したように上段
極板群1Eの温度は2時間目から上昇し始め、7時間目
に最高になって14時間目に熟成が終了するのに対し
て、下段極板群1Fはこれよりさらに遅く、4時間目よ
り温度が上昇して18時間目に熟成が終了した。そこで
18時間目に熟成を中止して活物質水分量を測定した結
果、図6に示すように上段極板群1Gが3.5%、下段
極板群1Hが4.8%であった。これは上段の極板群1
Gの方が速く熟成が完了したため、終了後若干乾燥が進
んだためである。また上段の極板群1Gのほうが下段極
板群1Hより速く熟成が進むものの実施例に比べると約
2倍以上の時間を要した。
Comparative Example For comparison, an electrode plate group constructed under the same conditions as in the above embodiment was placed in a conventional aging and drying chamber having the same dimensions as in the above embodiment, which was not provided with an air delivery nozzle, and was aged and dried. I did. In this case, the temperature, humidity, and amount of air to be put into the aging and drying chamber were the same as those in the above-mentioned examples. The stirring of the air in the aging drying chamber at this time was carried out by installing fans in the upper and side portions, as is generally done. In addition,
Here, the water content of the active material of the electrode plate before aging was also set to 10% as in the above example. As a result, as shown in FIG. 5, the temperature of the upper electrode plate group 1E begins to rise from the second hour, reaches the maximum at the seventh hour, and finishes aging at the 14th hour, while the lower electrode plate 1E is finished. Group 1F was slower than this, and the temperature rose from the 4th hour, and the aging was completed at the 18th hour. Therefore, as a result of stopping the aging at 18 hours and measuring the water content of the active material, the upper electrode group 1G was 3.5% and the lower electrode group 1H was 4.8% as shown in FIG. This is the upper plate group 1
This is because the ripening of G was completed faster and the drying was slightly advanced after the completion. Further, although the aging of the upper electrode group 1G progressed faster than that of the lower electrode group 1H, the time required was about twice as long as that of the example.

【0012】次に、上記実施例と同一の風量の100℃
の乾燥空気を熟成乾燥室に入れて乾燥を行なった結果、
上記実施例と同様に活物質中の水分量を0.5%以下に
するのに、上段極板群1Gで10時間、下段極板群1H
で16時間要した。この比較例は極板群を極板懸垂枠に
上下二段懸垂した場合の結果であるが、この懸垂段数を
増やすことにより、熟成時間および乾燥時間の極板群毎
のバラツキはさらに大きくなり、すべての極板群を熟成
乾燥させるには上記比較例よりさらに長くなることは言
うまでもない。
Next, at the same air flow rate as in the above embodiment, 100 ° C.
As a result of drying by putting the dry air of
As in the above example, in order to reduce the water content in the active material to 0.5% or less, the upper electrode plate group 1G was used for 10 hours and the lower electrode plate group 1H was used.
It took 16 hours. This comparative example is the result when the electrode plate group is vertically suspended in the electrode plate suspension frame by two stages, but by increasing the number of suspension stages, the variation for each electrode plate group of the aging time and the drying time is further increased, Needless to say, it takes longer than the comparative example to age and dry all the electrode plates.

【0013】[0013]

【発明の効果】上述したように、本発明による熟成乾燥
装置を用いることにより、熟成乾燥装置中の極板群に熟
成、あるいは乾燥に適した条件の空気を送出することに
より、極板懸垂枠に懸垂する極板群の量に関係なく懸垂
するすべての極板群をほぼ同一時間で短時間に熟成乾燥
が可能となる等工業的価値甚だ大なるものである。
As described above, by using the aging / drying apparatus according to the present invention, the electrode plate suspension frame can be delivered by sending air under conditions suitable for aging or drying to the electrode plate group in the aging / drying apparatus. Regardless of the amount of electrode plates suspended, it is possible to age and dry all electrode plates that are suspended in almost the same time in a short time, which is of great industrial value.

【図面の簡単な説明】[Brief description of drawings]

【図1】熟成乾燥室内にあって空気送出口を設けた空気
送出ノズルを極板群上部に配置した状態の一実施例を示
す説明図である。
FIG. 1 is an explanatory diagram showing an example of a state in which an air delivery nozzle provided with an air delivery port is disposed above an electrode plate group in an aging drying chamber.

【図2】極板群と空気送出ノズルとの位置関係の一実施
例を示す斜視概略説明図である。
FIG. 2 is a schematic perspective explanatory view showing an embodiment of the positional relationship between the electrode plate group and the air delivery nozzle.

【図3】図1に示す熟成乾燥装置を用いて最適条件で熟
成したときの極板温度の経時変化を示す曲線図である。
FIG. 3 is a curve diagram showing changes over time in the electrode plate temperature when aged under optimum conditions using the aged drying device shown in FIG.

【図4】図1に示す熟成乾燥装置を用いて乾燥したとき
の極板の活物質水分量の経時変化を示す曲線図である。
FIG. 4 is a curve diagram showing a change over time in the water content of the active material of the electrode plate when dried using the aging drying device shown in FIG. 1.

【図5】従来の熟成乾燥装置を用いて熟成したときの極
板温度の経時変化を示す曲線図である。
FIG. 5 is a curve diagram showing changes over time in electrode plate temperature when aged using a conventional aged drying device.

【図6】従来の熟成乾燥装置を用いて乾燥したときの極
板の活物質水分量の経時変化を示す曲線図である。
FIG. 6 is a curve diagram showing a change over time in the water content of the active material of the electrode plate when dried using a conventional aging dryer.

【符号の説明】[Explanation of symbols]

1は極板群、1A,1Cは上段極板群、1B,1Dは下
段極板群、2は極板懸垂枠、3は熟成乾燥室、4は空気
送出口、5は空気送出ノズル、6は空気調整機、7は空
気ポンプ。
1 is an electrode plate group, 1A and 1C are upper electrode plate groups, 1B and 1D are lower electrode plate groups, 2 is an electrode plate suspension frame, 3 is an aging drying chamber, 4 is an air delivery port, 5 is an air delivery nozzle, 6 Is an air conditioner and 7 is an air pump.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】ペーストを格子体に充填後の極板を重ね合
わせた極板群を極板懸垂枠に懸垂し、該懸垂各段の極板
に直接気体を当てるための空気送出ノズルを配置させる
ことを特徴とする鉛蓄電池用極板の熟成乾燥装置。
1. An air delivery nozzle for suspending an electrode plate group, which is obtained by stacking electrode plates after filling a grid body with paste, on an electrode plate suspension frame, and for directly applying gas to the electrode plates at each stage of the suspension. An aging / drying device for a lead-acid battery electrode plate, which is characterized by:
JP5071608A 1993-03-30 1993-03-30 Maturing/drying device of electrode plate for lead-acid battery Pending JPH06283160A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5071608A JPH06283160A (en) 1993-03-30 1993-03-30 Maturing/drying device of electrode plate for lead-acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5071608A JPH06283160A (en) 1993-03-30 1993-03-30 Maturing/drying device of electrode plate for lead-acid battery

Publications (1)

Publication Number Publication Date
JPH06283160A true JPH06283160A (en) 1994-10-07

Family

ID=13465540

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5071608A Pending JPH06283160A (en) 1993-03-30 1993-03-30 Maturing/drying device of electrode plate for lead-acid battery

Country Status (1)

Country Link
JP (1) JPH06283160A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100358443B1 (en) * 2000-08-23 2002-10-30 한국진공주식회사 A pole plate dryer of battery
CN102494521A (en) * 2011-12-06 2012-06-13 天能电池(芜湖)有限公司 Solidification chamber for accumulator grid plate
CN103943829A (en) * 2014-01-23 2014-07-23 超威电源有限公司 Lead acid storage battery plate humidifier
WO2015037581A1 (en) * 2013-09-12 2015-03-19 新神戸電機株式会社 Method for manufacturing paste-like electrode plate for lead storage cell, and electrode-plate-cleaning device used in said method
CN111966143A (en) * 2020-08-28 2020-11-20 界首市南都华宇电源有限公司 Storage battery electrode plate heating curing steam control device
CN112467089A (en) * 2020-11-25 2021-03-09 河北超威电源有限公司 Method and special equipment for solidifying and drying accumulator plate
CN114765255A (en) * 2022-04-01 2022-07-19 浙江超威贝特瑞科技有限公司 Accumulator plate curing chamber

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100358443B1 (en) * 2000-08-23 2002-10-30 한국진공주식회사 A pole plate dryer of battery
CN102494521A (en) * 2011-12-06 2012-06-13 天能电池(芜湖)有限公司 Solidification chamber for accumulator grid plate
WO2015037581A1 (en) * 2013-09-12 2015-03-19 新神戸電機株式会社 Method for manufacturing paste-like electrode plate for lead storage cell, and electrode-plate-cleaning device used in said method
JP5737487B1 (en) * 2013-09-12 2015-06-17 新神戸電機株式会社 Method of manufacturing paste type electrode plate for lead acid battery and electrode plate cleaning device used in the method
GB2533976A (en) * 2013-09-12 2016-07-13 Shin-Kobe Electric Machinery Co Ltd Method for manufacturing paste-like electrode plate for lead storage cell, and electrode-plate-cleaning device used in said method
GB2533976B (en) * 2013-09-12 2021-04-07 Shin Kobe Electric Machinery Co Ltd Method of manufacturing paste-type electrode for lead-acid battery and cleaning apparatus of electrode for use with the method
CN103943829A (en) * 2014-01-23 2014-07-23 超威电源有限公司 Lead acid storage battery plate humidifier
CN111966143A (en) * 2020-08-28 2020-11-20 界首市南都华宇电源有限公司 Storage battery electrode plate heating curing steam control device
CN112467089A (en) * 2020-11-25 2021-03-09 河北超威电源有限公司 Method and special equipment for solidifying and drying accumulator plate
CN114765255A (en) * 2022-04-01 2022-07-19 浙江超威贝特瑞科技有限公司 Accumulator plate curing chamber

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